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MOST SIGNIFICANT RESEARCH CONTRIBUTIONS
2. Henni A. , D. Lal and Mather A.E.,
Equilibrium Solubility of Ethane in Triethylene Glycol Monomethyl Ether, Can. J. Chem. Eng., 74(3), 423-425
(1996). 3. Henni A., D. Lal, and Mather A.E., Equilibrium Solubility of Ethane in
NMP, Can. J. Chem. Eng., 74, 423-425, (1996). 4. Henni A. and Mather A. E., Solubility of CO2, N2O,
CH4, C2H6 in Polar Solvents, J. Can. Pet. Tech.,
Nov. 1999 (special issue). 5. Henni A. and A.E. Mather Solubility of Methane in Polar
Solvents, Submitted to The Industrial & Engineering Chemistry Research Journal. 6. Henni A., P. Tontiwachwuthikul, A.
Chakma, Solubility of CO2 in Fourteen Polar Solvents at temperatures from
25 °C to 60 °C, Manuscript to be
Submitted to J. Chem. Eng. Data. 7. Henni A., P. Tontiwachwuthikul, A.
Chakma,
Solubility of Methane and Ethane in Five Promising Solvents For Natural Gas
Sweetening at temperatures from 25 °C to 60 °C, Manuscript to be Submitted to J. Chem. Eng. Data. 8. Henni
A., J.
Carroll and Mather A.E., Vapor-Liquid-Liquid Locus of the system CO2-
Water", Manuscript in preparation. Most of the
high-pressure solubility work was done when the applicant was at the University of
Alberta. Since joining the University of Regina, he has started building a solubility
program to screen a large number of physical solvents for their capacity for CO2. A simple solubility model based on a modification
of the Solubility parameter theory was developed to predict the solubility of CO2,
methane and ethane in any physical solvent and at any temperature if the solubility in one
solvent is known at a given temperature. (b) Physical and Transport Properties Measurement and
Modeling 1. Henni A., P. Tontiwachwuthikul, A. Chakma and
Mather A. E., Densities and Viscosities
for Binary Mixtures of Triethylene Glycol Monomethyl Ether and Water in the Interval 25
°C to 80 °C, J. Chem. Eng. Data, 44,
101-107 (1999).\ 2. Henni A., Y. Maham, P. Tontiwachwuthikul, A.
Chakma and Mather A. E., Densities and Viscosities for Binary Mixtures of
Triethylene Glycol Monomethyl Ether and N-Methyldiethanolamine from 25 °C to 70 °C and
N-Methyldiethanolamine + Ethanol at 40 °C, J. Chem. Eng. Data, 45, 247-253, 2000. 3. Henni A., P. Tontiwachwuthikul, A. Chakma and
Mather A. E., Volumetric Properties and Viscosities for Aqueous Diglycolamine
Solutions from 25 °C to 70
°C, J. Chem. Eng. Data, 47, 124-130,
2000. 4. Henni A., Hromek, J. J., P. Tontiwachwuthikul, A.
Chakma, Volumetric Properties and Viscosities of Aqueous AMP from 25 °C to 70
°C, In Press, J. Chem. Eng. Data. 5. Henni A., P. Tontiwachwuthikul, A. Chakma,
Volumetric Properties and Viscosities of Aqueous Tetraethylene Glycol Dimethyl Ether
from 25 °C to 70 °C, Manuscript to be
Submitted to J. Chem. Data. 6. Henni A., P. Tontiwachwuthikul, A. Chakma,
Volumetric Properties and Viscosities of Aqueous N-Formyl Morpholine from 25 °C to
70 °C, Manuscript to be Submitted to J.
Chem. Data.
1) Henni A., P. Tontiwachwuthikul and A. Chakma, Kinetics of CO2 Absorption
with Chemical Reactions in Mixed Solvents: A Comprehensive Review, 47th Canadian
Chemical Engineering Conference, Edmonton, October 7-10, 1997.
The kinetics studies were initiated after building an acrylic cell reactor. It is the
intent of the author to investigate the effect of different polar solvents on the
absorption of CO2 in tertiary amines. Dr. Henni has proven that there is an
obvious and substantial enhancement of the absorption rate of CO2 in MDEA in the presence of polar
solvents. This is in contradiction with what is published in the literature. Dr. Henni
also plans to measure CO2 absorption in alkanolamines with more than one amine
group. Research work has shown that the addition of a physical solvent enhanced the
absortion rate of a mixed solvent over its aqueous alkanolamine counterpart.The kinetics
work is still in progress.
(d) Calorimetry
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